JPH0832303B2 - Carbon dioxide immobilization method - Google Patents

Carbon dioxide immobilization method

Info

Publication number
JPH0832303B2
JPH0832303B2 JP1313485A JP31348589A JPH0832303B2 JP H0832303 B2 JPH0832303 B2 JP H0832303B2 JP 1313485 A JP1313485 A JP 1313485A JP 31348589 A JP31348589 A JP 31348589A JP H0832303 B2 JPH0832303 B2 JP H0832303B2
Authority
JP
Japan
Prior art keywords
carbon dioxide
dioxide hydrate
seawater
hydrate
pressure
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP1313485A
Other languages
Japanese (ja)
Other versions
JPH03177311A (en
Inventor
正樹 飯島
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP1313485A priority Critical patent/JPH0832303B2/en
Priority to EP90250288A priority patent/EP0429154B1/en
Priority to CA002030391A priority patent/CA2030391C/en
Priority to DE69015326T priority patent/DE69015326T2/en
Priority to KR1019900018896A priority patent/KR930008446B1/en
Publication of JPH03177311A publication Critical patent/JPH03177311A/en
Priority to US07/790,148 priority patent/US5304356A/en
Priority to US08/028,602 priority patent/US5364611A/en
Publication of JPH0832303B2 publication Critical patent/JPH0832303B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/141Feedstock

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  • Treating Waste Gases (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Carbon And Carbon Compounds (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は二酸化炭素の固定化法に関し、特に大気中の
二酸化炭素による地球の温暖化等の環境破壊を防止する
ために二酸化炭素を固定化する方法に関する。
TECHNICAL FIELD The present invention relates to a carbon dioxide immobilization method, and in particular, immobilizes carbon dioxide to prevent environmental destruction such as global warming due to carbon dioxide in the atmosphere. On how to do.

〔従来の技術〕[Conventional technology]

発電所や一般産業用ボイラ等での化石燃料の燃焼によ
り、大気中の二酸化炭素濃度が増し、近年温室効果と呼
ばれている地球の温暖化現象が問題視されることとなっ
た。この大気中の二酸化炭素の濃度の増加を防止するた
め二酸化炭素を大気に放出せずに投棄する方法、または
二酸化炭素を大気から回収した後投棄する方法として、
下記の方法が報告されている。
Combustion of fossil fuels in power plants, boilers for general industries, etc. has increased the carbon dioxide concentration in the atmosphere, and in recent years the global warming phenomenon called the greenhouse effect has become a problem. As a method of discarding carbon dioxide without releasing it to the atmosphere to prevent an increase in the concentration of carbon dioxide in the atmosphere, or as a method of discarding carbon dioxide after recovering it from the atmosphere,
The following methods have been reported.

1) 二酸化炭素を海水に溶解させ海洋に投棄する。二
酸化炭素が溶解した海水は周囲の海水より比重が大きい
ため、海洋底へ沈んでいく。
1) Dissolve carbon dioxide in seawater and dump it in the ocean. The seawater in which carbon dioxide is dissolved has a larger specific gravity than the surrounding seawater, so it sinks to the ocean floor.

2) 液体二酸化炭素は深さ3,000m以上の深海における
温度・圧力下では周囲の海水よりも比重が大きいため、
液体二酸化炭素として深海3,000m以上のところに投棄す
る。
2) Since liquid carbon dioxide has a larger specific gravity than the surrounding seawater under the temperature and pressure in the deep sea with a depth of 3,000 m or more,
Discard as liquid carbon dioxide in the deep sea more than 3,000m.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

前項に挙げた従来の方法1)では、二酸化炭素を溶解
した海水は海洋での海水の流れにより広い範囲に拡散
し、海洋生物の生態系に影響を与えるおそれがある。ま
た、従来の方法2)では、二酸化炭素を液化し、さらに
その液体二酸化炭素を深海3,000m以上のところまで導く
ための大きな動力が必要であり、従来の方法1)と同様
に海洋中に広く拡散するおそれもある。
In the conventional method 1) mentioned in the preceding paragraph, seawater in which carbon dioxide is dissolved may spread over a wide range due to the flow of seawater in the ocean, which may affect the ecosystem of marine organisms. In addition, the conventional method 2) requires large power for liquefying carbon dioxide and further guiding the liquid carbon dioxide to a depth of 3,000 m or more in the deep sea. May spread.

以上の従来の技術水準に鑑み、本発明は燃焼排ガス中
や大気中から回収した二酸化炭素を海水中あるいは淡水
中に拡散することなく、また海洋生物の生態系に影響を
与えることなく、安全に安定的に二酸化炭素を固定する
方法を提供しようとするものである。
In view of the above-mentioned conventional state of the art, the present invention does not diffuse carbon dioxide recovered from the combustion exhaust gas or the atmosphere into seawater or freshwater, and does not affect the ecosystem of marine organisms safely. It is intended to provide a method of stably fixing carbon dioxide.

〔課題を解決するための手段〕[Means for solving the problem]

本発明は二酸化炭素を二酸化炭素ハイドレイト生成に
必要な圧力、温度下で海水又は淡水と接触させて二酸化
炭素ハイドレイトを生成させ、二酸化炭素ハイドレイト
が安定な条件下にある海水中または淡水中に沈めること
を特徴とする二酸化炭素の固定化法である。
The present invention is to produce carbon dioxide hydrate by contacting carbon dioxide with seawater or fresh water under the pressure and temperature required for carbon dioxide hydrate formation, and the carbon dioxide hydrate is under stable conditions in seawater or freshwater. It is a carbon dioxide immobilization method characterized by being immersed in

まず第1図により二酸化炭素ハイドレイトが生成する
圧力と温度の関係を説明する。
First, the relationship between the pressure generated by carbon dioxide hydrate and the temperature will be described with reference to FIG.

第1図においてKV-S値は二酸化炭素ハイドレイトの平
衡データであり、このKV-S値が1.0以下になる圧力と温
度において二酸化炭素ハイドレイトが生成される条件が
満たされる。
In FIG. 1, the K VS value is the equilibrium data of carbon dioxide hydrate, and the conditions for generating carbon dioxide hydrate are satisfied at the pressure and temperature at which this K VS value becomes 1.0 or less.

また第1表は一般的な海洋において二酸化炭素ハイド
レイトの生成する水深と温度との関係を示したものであ
る。水深が深ければ圧力が高いので、それに対応する水
温は高くても二酸化炭素ハイドレイトを生成することが
できる。
Table 1 shows the relationship between the water depth and temperature at which carbon dioxide hydrate is generated in the general ocean. If the water depth is deep, the pressure is high, so carbon dioxide hydrate can be generated even if the water temperature corresponding to it is high.

次に、二酸化炭素ハイドレイトおよび海水の比重につ
いて説明する。
Next, the specific gravity of carbon dioxide hydrate and seawater will be described.

二酸化炭素ハイドレイトの比重は1.129程度であり、
温度や圧力にほとんど影響されないことがわかってい
る。また、海水の大気圧における比重は1.03程度であ
り、淡水の比重は、それよりも小さい。また水深が増
し、圧力が増しても、水の比重の増加量は小さく、二酸
化炭素ハイドレイトの比重に対し無視できる。これによ
り生成された二酸化炭素ハイドレイトを海水中または淡
水中に放置すれば自然に沈下し、海洋であれば海底に堆
積し、安定かつ安定的に二酸化炭素を固定することがで
きる。
The specific gravity of carbon dioxide hydrate is about 1.129,
It is known that it is hardly affected by temperature and pressure. The specific gravity of seawater at atmospheric pressure is about 1.03, and the specific gravity of fresh water is smaller than that. Even if the water depth increases and the pressure increases, the increase in the specific gravity of water is small and can be ignored with respect to the specific gravity of carbon dioxide hydrate. If the carbon dioxide hydrate thus produced is left in seawater or fresh water, it will sink naturally, and if it is an ocean, it will be deposited on the seabed and carbon dioxide can be fixed stably and stably.

〔作用〕[Action]

二酸化炭素を昇圧し、二酸化炭素ハイドレイトが生成
する圧力と温度条件を満たす海水中あるいは淡水中に
て、海水あるいは淡水と混合し、二酸化炭素ハイドレイ
トを生成させる。二酸化炭素ハイドレイトは比重が1.12
9程度と海水や淡水の比重に比べ大きいため水底に沈
む。海洋中に置く場合は、海域により違いはあるが日本
近海においては200〜500mより深い海中において、二酸
化炭素ハイドレイトが生成する圧力、温度条件を満たし
ている。
Carbon dioxide is pressurized and mixed with seawater or fresh water in seawater or freshwater satisfying the pressure and temperature conditions for producing carbon dioxide hydrate to generate carbon dioxide hydrate. Carbon dioxide hydrate has a specific gravity of 1.12
Since it is about 9 which is larger than the specific gravity of seawater or freshwater, it sinks to the bottom of the water. When placed in the ocean, it varies depending on the sea area, but in the sea near Japan, deeper than 200 to 500 m, the pressure and temperature conditions for carbon dioxide hydrate formation are satisfied.

第2図は日本近海海域における2月の水温の鉛直分布
を示す。○印は潮岬の南約100kmの北緯32.5゜、東経13
5.5゜の黒潮域、△印は鳥取の北約200kmの北緯37.5゜、
東経134.5゜の対馬海流域、□印は襟裳岬の南東約150km
の北緯41.5゜、東経144.5゜の親潮域を示す。
Figure 2 shows the vertical distribution of water temperature in February in the waters around Japan. ○ indicates 32.5 ° north latitude and 13 east longitude approximately 100km south of Cape Shio
Kuroshio region at 5.5 °, △ indicates 37.5 ° north latitude about 200km north of Tottori,
Tsushima Sea basin at 134.5 ° east longitude, □ indicates approximately 150km southeast of Cape Erimo
Shows the Oyashio region at 41.5 ° north latitude and 144.5 ° east longitude.

第2図において斜線を施した所は、第1表により二酸
化炭素ハイドレイトが生成する範囲を示す。第2図によ
れば、日本の2月では北緯41.5゜、東経144.5゜の海域
においては120mより深い水深において、北緯37.5゜、東
経134.5゜の海域においては220mより深い水深におい
て、また北緯32.5゜、東経135.5゜の海域においては500
mより深い水深においてそれぞれ二酸化炭素ハイドレイ
トの生成が可能である。
The shaded area in FIG. 2 indicates the range in which carbon dioxide hydrate is produced according to Table 1. According to Fig. 2, in February in Japan, at a latitude of 41.5 ° N, 144.5 ° east, at a depth of more than 120 m, at a latitude of 37.5 ° N, at a depth of 134.5 °, at a depth of more than 220 m, and a latitude of 32.5 ° , 500 in the sea area of 135.5 ° east longitude
It is possible to generate carbon dioxide hydrate at depths deeper than m.

第3図は第2図と同様の日本近海三海域における8月
の水温の鉛直分布を示す。
Fig. 3 shows the vertical distribution of water temperature in August in the three waters around Japan similar to Fig. 2.

第3図において斜線を施したところは、第1表により
二酸化炭素ハイドレイトが生成する範囲を示す。第3図
によれば、日本の8月では北緯41.5゜、東経144.5゜の
海域においては160mより深い水深において二酸化炭素ハ
イドレイトの生成が可能であり、北緯37.5゜東経134.5
゜の海域においては220mより深い水深で、北緯32.5゜東
経135.5゜の海域においては450mより深い水深において
それそれ二酸化炭素ハイドレイトの生成が可能である。
The shaded area in FIG. 3 indicates the range in which carbon dioxide hydrate is produced according to Table 1. According to Fig. 3, carbon dioxide hydrates can be produced at a depth of more than 160m in the sea area of 41.5 ° north latitude and 144.5 ° east longitude in August of Japan, and 37.5 ° north latitude and 134.5 east longitude 134.5.
It is possible to generate carbon dioxide hydrate at a depth of more than 220 m in the sea area of ゜, and at a depth of more than 450 m in the sea area of latitude 32.5 ゜ north and 135.5 ℃ east longitude.

第2図、第3図にて示されるように、海底は海の上部
と比較し、二酸化炭素ハイドレイトにとってはより安定
した条件を満たしている。このため海底に堆積した二酸
化炭素ハイドレイトは安定した状態に保たれる。
As shown in Fig. 2 and Fig. 3, the seabed satisfies more stable conditions for carbon dioxide hydrate as compared with the upper part of the sea. Therefore, the carbon dioxide hydrate deposited on the seabed is kept stable.

二酸化炭素ハイドレイトを地上または海上にて生成さ
せ、海中に投棄することも可能である。この場合、生成
された二酸化炭素ハイドレイトは、安定した条件を備え
た海中に導くまで溶解または気化しないよう保持し、さ
らに安定した温度、圧力条件を備えた海水中に二酸化炭
素ハイドレイトを沈ませ、海底に堆積させれば、二酸化
炭素ハイドレイトは安定した状態に海底に保持される。
It is also possible to generate carbon dioxide hydrate on the ground or at the sea and dump it into the sea. In this case, the generated carbon dioxide hydrate is kept so that it does not melt or vaporize until it is introduced into the sea with stable conditions, and the carbon dioxide hydrate is submerged in seawater with stable temperature and pressure conditions. , If it is deposited on the seabed, the carbon dioxide hydrate will be retained on the seabed in a stable state.

〔実施例1〕 本発明の実施例1を第4図及び第2表によって説明す
る。
Example 1 Example 1 of the present invention will be described with reference to FIG. 4 and Table 2.

二酸化炭素ガス1を昇圧機2にて25kg/cm2ゲージ圧ま
で昇圧し、北緯41.5゜東経144.5゜の水域において200m
の水深に設置された二酸化炭素ハイドレイト生成器4へ
導く。二酸化炭素ハイドレイト生成器4の設置される水
深の海水5の温度は、2月は2℃、8月は3℃であり、
二酸化炭素ハイドレイトが生成するに十分な温度、圧力
条件を備えている。二酸化炭素ハイドレイト生成器4に
て生成された二酸化炭素ハイドレイトは、海水中を沈
み、海底に堆積する。
Carbon dioxide gas 1 is boosted to 25 kg / cm 2 gauge pressure by booster 2 and 200 m in the water area of north latitude 41.5 ° east longitude 144.5 °
To the carbon dioxide hydrate generator 4 installed at the water depth. The temperature of the seawater 5 at the depth where the carbon dioxide hydrate generator 4 is installed is 2 ° C in February and 3 ° C in August,
It has sufficient temperature and pressure conditions to generate carbon dioxide hydrate. The carbon dioxide hydrate generated by the carbon dioxide hydrate generator 4 sinks in seawater and is deposited on the seabed.

〔実施例2〕 本発明の実施例2を第5図および第3表において説明
する。
Example 2 Example 2 of the present invention will be described with reference to FIG. 5 and Table 3.

二酸化炭素ガス1を昇圧機2にて25kg/cm2ゲージ圧ま
で昇圧し、冷却器4にて3℃まで冷却してライン5より
二酸化炭素ハイドレイト生成機に導き、一方3℃の淡水
または海水6を20kg/cm2ゲージ圧までポンプ7にて昇圧
し、二酸化炭素ハイドレイト生成器9に導き、二酸化炭
素ハイドレイトを生成させる。この二酸化炭素ハイドレ
イトを二酸化炭素ハイドレイト運搬機11及び二酸化炭素
ハイドレイトの海水中への下降管12を通して、二酸化炭
素ハイドレイトの状態を保持しながら北緯41.5゜東経14
4.5゜の海域の水深200mまで導く。この海域の水深200m
は2月は2℃、8月は3℃であり、二酸化炭素ハイドレ
イトの安定な状態にあり、二酸化炭素ハイドレイトは海
中を沈み、海底に堆積し、安定な状態に保たれる。
Carbon dioxide gas 1 is boosted to 25 kg / cm 2 gauge pressure by booster 2 , cooled to 3 ° C by cooler 4 and led to carbon dioxide hydrate generator from line 5, while freshwater or seawater at 3 ° C. The pressure of 6 is increased to 20 kg / cm 2 gauge pressure by the pump 7, and is guided to the carbon dioxide hydrate generator 9 to generate carbon dioxide hydrate. This carbon dioxide hydrate is passed through the carbon dioxide hydrate carrier 11 and the descending pipe 12 of the carbon dioxide hydrate into seawater, while maintaining the state of the carbon dioxide hydrate 41.5 ° north latitude 14 ° E
It leads to a water depth of 200 m in the 4.5 ° area. 200m depth of water in this area
The temperature is 2 ° C in February and 3 ° C in August, and the carbon dioxide hydrate is in a stable state. The carbon dioxide hydrate sinks in the sea, accumulates on the seabed, and is kept stable.

〔発明の効果〕〔The invention's effect〕

以上の説明のように、本発明の二酸化炭素を固定する
方法は、燃焼排ガス中や大気中の二酸化炭素を回収し、
大気中の二酸化炭素の増加を防止するにあたり、従来の
方法である回収した二酸化炭素を海水に溶解し、あるい
は液体二酸化炭素として海洋に投棄する方法に対し、海
洋または淡水中に拡散させずに二酸化炭素ハイドレイト
として一定箇所に安定的に堆積しておくことができるた
め、海洋または淡水の生態系への影響を防止できる。
As described above, the method for fixing carbon dioxide of the present invention collects carbon dioxide in the combustion exhaust gas and the atmosphere,
In order to prevent the increase of carbon dioxide in the atmosphere, compared with the conventional method of dissolving recovered carbon dioxide in seawater or discarding it as liquid carbon dioxide into the ocean, carbon dioxide is not diffused in the ocean or fresh water. Since it can be stably deposited as carbon hydrate in certain places, it can prevent the impact on the ecosystem of the ocean or freshwater.

また、液体二酸化炭素として海洋または淡水に投棄す
る方法に比べ、海水または淡水中に投入するための動力
を大幅に削減でき、大量の二酸化炭素の固定に有効であ
る。
Further, compared with the method of dumping as liquid carbon dioxide into the ocean or fresh water, the power for throwing into sea water or fresh water can be significantly reduced, and it is effective for fixing a large amount of carbon dioxide.

【図面の簡単な説明】[Brief description of drawings]

第1図は二酸化炭素ハイドレイトの平衡図、第2図は2
月における日本近海の水温の鉛直分布と二酸化炭素ハイ
ドレイト生成範囲を示す図表、第3図は8月における日
本近海の水温の鉛直分布と二酸化炭素ハイドレイト生成
範囲を示す図表、第4図は本発明の第1実施例の説明
図、第5図は本発明の第2実施例の説明図である。
Fig. 1 shows the equilibrium diagram of carbon dioxide hydrate, and Fig. 2 shows 2
Chart showing the vertical distribution of water temperature in the waters near Japan and the range of carbon dioxide hydrate formation in March, Fig. 3 is the chart showing the vertical distribution of water temperatures in the waters near Japan in August, and the range of carbon dioxide hydrate formation, and Fig. 4 is the book FIG. 5 is an explanatory diagram of a first embodiment of the invention, and FIG. 5 is an explanatory diagram of a second embodiment of the present invention.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】二酸化炭素を二酸化炭素ハイドレイト生成
に必要な圧力、温度下で海水又は淡水と接触させて二酸
化炭素ハイドレイトを生成させ、二酸化炭素ハイドレイ
トが安定な条件下にある海水中または淡水中に沈めるこ
とを特徴とする二酸化炭素の固定化法。
1. A method for producing carbon dioxide hydrate by contacting carbon dioxide with seawater or fresh water under the pressure and temperature required for producing carbon dioxide hydrate, wherein the carbon dioxide hydrate is stable in seawater or A carbon dioxide immobilization method characterized by being immersed in fresh water.
JP1313485A 1989-11-21 1989-12-04 Carbon dioxide immobilization method Expired - Fee Related JPH0832303B2 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP1313485A JPH0832303B2 (en) 1989-12-04 1989-12-04 Carbon dioxide immobilization method
EP90250288A EP0429154B1 (en) 1989-11-21 1990-11-20 Method for the fixation of carbon dioxide and apparatus for the treatment of carbon dioxide
CA002030391A CA2030391C (en) 1989-11-21 1990-11-20 Method for the fixation of carbon dioxide, apparatus for fixing and disposing carbon dioxide, and apparatus for the treatment of carbon dioxide
DE69015326T DE69015326T2 (en) 1989-11-21 1990-11-20 Method for fixing carbon dioxide and device for treating carbon dioxide.
KR1019900018896A KR930008446B1 (en) 1989-11-21 1990-11-21 Method of fixing carbon dioxide and apparatus for dumping carbon dioxide and apparatus for treating carbon dioxide
US07/790,148 US5304356A (en) 1989-11-21 1991-11-08 Method for the fixation of carbon dioxide, apparatus for fixing and disposing carbon dioxide, and apparatus for the treatment of carbon dioxide
US08/028,602 US5364611A (en) 1989-11-21 1993-03-08 Method for the fixation of carbon dioxide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1313485A JPH0832303B2 (en) 1989-12-04 1989-12-04 Carbon dioxide immobilization method

Publications (2)

Publication Number Publication Date
JPH03177311A JPH03177311A (en) 1991-08-01
JPH0832303B2 true JPH0832303B2 (en) 1996-03-29

Family

ID=18041877

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1313485A Expired - Fee Related JPH0832303B2 (en) 1989-11-21 1989-12-04 Carbon dioxide immobilization method

Country Status (1)

Country Link
JP (1) JPH0832303B2 (en)

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* Cited by examiner, † Cited by third party
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WO2002002460A2 (en) * 2000-06-29 2002-01-10 Exxonmobil Research And Engineering Company Heat exchanged membrane reactor for electric power generation
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